Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/36—Selection of substances as active materials, active masses, active liquids
  • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
  • H01M4/485—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B82—NANOTECHNOLOGY
  • B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
  • B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
• • H—ELECTRICITY
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  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M10/00—Secondary cells; Manufacture thereof
  • H01M10/05—Accumulators with non-aqueous electrolyte
  • H01M10/052—Li-accumulators
  • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
• • H—ELECTRICITY
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  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/04—Processes of manufacture in general
  • H01M4/0402—Methods of deposition of the material
  • H01M4/0404—Methods of deposition of the material by coating on electrode collectors
• • H—ELECTRICITY
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  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
  • H01M4/133—Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
  • H01M4/139—Processes of manufacture
  • H01M4/1393—Processes of manufacture of electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/36—Selection of substances as active materials, active masses, active liquids
  • H01M4/362—Composites
  • H01M4/364—Composites as mixtures
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/36—Selection of substances as active materials, active masses, active liquids
  • H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/36—Selection of substances as active materials, active masses, active liquids
  • H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
  • H01M4/387—Tin or alloys based on tin
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/02—Electrodes composed of, or comprising, active material
  • H01M4/36—Selection of substances as active materials, active masses, active liquids
  • H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
  • H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
  • H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/10—Energy storage using batteries

Definitions

• the present invention relates in general to the development of novel composite materials, and more particularly, to the development and use of novel nanocomposite anode materials to replace the carbon anode in lithium ion cells.
• Lithium ion batteries have become the choice of power source for portable electronic devices such as cell phones, laptops, and PDAs due to their higher energy density compared to other rechargeable systems. They are also being intensively pursued for plug-in hybrid electric vehicles (PHEV) and electric vehicles (EV). Lithium ion batteries currently use graphite as the anode due to its excellent cycling behavior. However, the currently used carbon anode has the drawbacks of limited capacity (372 mAh/g) and safety concerns.
• an electrode for a lithium battery that includes (a) an electrochemically active metal element which, prior to cycling, is in the form of an intermetallic compound or an elemental metal and (b) a non- electrochemically active metal element.
• the electrode has high initial capacities that are retained even after repeated cycling. The electrode also exhibits high coulombic efficiencies.
• United States Patent Number 6,949,312 issued to Kawakami and Asao (2005) discloses an electrode material for an anode of a rechargeable lithium battery, containing a particulate comprising an amorphous Sn-A-X alloy with a substantially non-stoichiometric ratio composition.
• A indicates at least one kind of an element selected from a group consisting of transition metal elements
• X indicates at least one kind of an element selected from a group consisting of O, F, N, Mg, Ba, Sr, Ca, La, Ce, Si, Ge, C, P, B, Pb, Bi, Sb, Al, Ga, In, Tl, Zn, Be, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu, As, Se, Te, Li and S, where the element X is not always necessary to be contained. Disclosure of the Invention
• the present invention provides a Sn-MC x -C nanostructured anode composition exhibiting excellent capacity retention with high capacity and rate capability having a Sn-MC x -C anode composition that alleviates the volume expansion encountered with alloy anodes during the charge-discharge process, wherein x is between 0.01 and 4 and M is selected from the group consisting of Ti, V, Cr, Mn, Fe, Mo, W, Al, Si, or combinations thereof.
• the Sn-MC x -C anode composition includes TiC, Fe 3 C, SiC and may or may not include one or more dopants to form a doped Sn-MC x -C anode composition.
• the present invention also provides a Sb-MO x -C nanostructured anode composition exhibiting excellent capacity retention with high capacity and rate capability having a Sb-MO x -C anode composition that alleviates the volume expansion encountered with alloy anodes during the charge-discharge process, wherein x is between 0.1 and 3 and M is selected from the group consisting of Al, Mg, Ti, V, Cr, Mn, Fe, Co, Ni, Zr, Mo, W, Nb, Ta, or combinations thereof.
• the Sb-MO x -C anode composition having Al 2 O 3 , TiO 2 , MoO 3 and may or may not include one or more dopants to form a doped Sn-MO x -C anode composition.
• the present invention provides a method of making a Sb-MO x -C nanocomposite by providing a nanocomposite comprising a Sb 2 O 3 source, a M source, and a C source; milling the nanocomposite by a high-energy mechanical milling process to form a Sb-MO x -C nanocomposite having a nanostructured Sb dispersion in a matrix of an amorphous M-oxide and a conductive carbon.
• the M source is Al and the amorphous M-oxide is Al 2 O 3 ; M source is Ti and the amorphous M-oxide is TiO 2 ; or the M source is Mo and the amorphous M-oxide is MoO 3 .
• the C source may include acetylene black, graphene, graphite, hard carbon, or other forms of carbon or carbon containing precursors like glucose and sucrose.
• the present invention provides a method of making a Sn-MC x -C nanocomposite by heating a mixture of a Sn source and a M source; and milling the Sn-M with a carbon source by a high- energy mechanical milling process to form a Sn-MC x -C nanocomposite dispersion.
• the M source is Ti to form a Sn-TiC x -C nanocomposite; the M source is V to form a Sn-VC x -C nanocomposite; the M source is Cr to form a Sn-CrC x -C nanocomposite; the M source is Mn to form a Sn-MnC x -C nanocomposite; the M source is Fe to form a Sn-FeC x -C nanocomposite; the M source is Mo to form a Sn-MoC x -C nanocomposite; the M source is W to form a Sn-WC x -C nanocomposite; the M source is Al to form a Sn-AlC x -C nanocomposite; or the M source is Si to form a Sn-SiC x -C nanocomposite.
• the present invention provides a method of making a Sn-MC x -C electrode by forming a Sn-
• MC x -C nanocomposite by heating a mixture of a Sn source and a M source and milling the mixture with a carbon source by a high-energy mechanical milling process to form a Sn-MC x -C nanocomposite; mixing a slurry of a carbon black source, a polyvinylidene fluoride source, and Sn-MC x -C nanocomposite in N-methylpyrrolidinone; coating the slurry on a substrate; and curing the slurry coating to form a Sn-MC x -C electrode.
• the M source may be selected from the group consisting of Ti, V, Cr, Mn, Fe, Mo, W, Al, Si, or combinations thereof.
• the present invention provides a method of making a Sb-MO x -C electrode by forming a Sb-
• MO x -C nanocomposite by milling a Sb 2 O 3 source, a M source, and a C source to form a Sb- MO x -C nanocomposite; mixing a slurry of a carbon black source, a polyvinylidene fluoride source, Sb-MO x -C nanocomposite in N-methylpyrrolidinone; coating the slurry on a substrate; and curing the slurry coating to form a Sb-MO x -C electrode.
• M may be selected from the group consisting of Al, Mg, Ti, V, Cr, Mn, Fe, Co, Ni, Zr, Mo, W, Nb, Ta, or combinations thereof.
• FIGURE 1 shows the synthetic scheme employed to obtain the Sn-TiC-C nanocomposite
• FIGURE 3a shows STEM images and
• FIGURE 3b shows TEM images of the Sn-TiC-C nanocomposite. Also shown are the fast Fourier transform images over selected regions;
• FIGURE 4a shows STEM images
• FIGURE 4b shows HRTEM images of the Sb-MO x -C (M
• FIGURE 5 shows the XRD patterns of the Sn-Ti alloy and Sn-TiC-C nanocomposite
• FIGURE 7 is the XPS spectra of the Sn-TiC-C nanocomposite showing the Sn 3d, Ti 2p, and C
• FIGURE 9 depicts the Raman spectrum of the Sn-TiC-C nanocomposite
• FIGURE 10a shows the discharge-charge profiles and FIGURE 10b shows differential capacity plots (DCP) of the Sn-TiC-C nanocomposites.
• the inset in FIGURE 10a shows the first discharge-charge profiles of milled carbon (acetylene black) cycled at a rate of C/2;
• FIGURE 1 Ia is a comparison of the discharge-charge profiles and
• FIGURE 12a shows the comparison of the cycling performances of Sn-TiC-C nanocomposite with those of Sn, Sn-C, and Sn-Ti and
• FIGURE 12b shows the cycling performances of Sn-TiC- C nanocomposite in presence of 150 ppm and 300 ppm Mn 2+ in the electrolyte.
• the inset in FIGURE 12a shows the discharge capacity of Sn-TiC
• EIS electrochemical impedance spectra
• the nanocomposites are prepared by mechanochemical (ball milling) method.
• the MC x -C or MO x -C present in the nanocomposite anode of the present invention act as a buffer to accommodate volume changes thereby alleviating the huge volume expansion encountered with alloy anodes during the charge-discharge process.
• the nanocomposite anode materials of the present invention have an excellent cycle life and overcomes the problem of degradation in electrochemical performance during cycling that is seen with the traditional alloy anodes that are used in lithium ion batteries.
• lithium alloy anode materials Li x M 3 have attracted much attention due to their high capacity values.
• These alloy anodes also offer an added advantage of better safety than graphite due to their operating voltage well above that of LiZLi + and less surface reactivity with the electrolyte.
• Antimony alloys are appealing as they offer high theoretical capacity (gravimetric and volumetric) and an operating voltage well above that of metallic lithium.
• the reaction of Sb with lithium to form Li 3 Sb is accompanied by a large volume change of 137 percent, 15"19 which results in cracking and crumbling of the alloy particles, disconnection of the electrical contact between the particles and current collectors, and consequent capacity fade during cycling.
• Sb-containing intermetallic compounds such as Cu 2 Sb, 21 CoSb, 22 CrSb, 23 and MnSb, 24 in which only Sb is electrochemically active, SnSb, 14 ' 25"26 InSb, 27 Zn 4 Sb 3 , 28 and AlSb, 29 in which both the metals are electrochemically active with different lithium reaction mechanisms, have been pursued.
• SnSb, 14 ' 25"26 InSb, 27 Zn 4 Sb 3 , 28 and AlSb, 29 in which both the metals are electrochemically active with different lithium reaction mechanisms.
• most of these intermetallic alloy anodes still exhibit capacity fade.
• the use of these alloy anodes in practical lithium ion cells has been plagued by severe capacity fade, arising from a huge volume change occurring during the charge-discharge (lithium alloying/dealloying) process.
• the volume change leads to lattice stress and consequent cracking and crumbling of the alloy particles during cycling, resulting in abrupt loss in capacity within a few charge-discharge cycles. 7 ' 30
• significant effort has been focused on buffering the volume expansion by using nanostructured materials and active- inactive composite materials.
• the nanostructured materials are expected to offer shorter diffusion length for lithium ions and accommodate the strain occurring during cycling, 2 ' 12 ' 31 the large surface-to-volume ratio and the high surface reactivity pose difficulties.
• the active- inactive composite strategy involves a mixture of two materials, one reacting with lithium while the other acting as an electrochemically inactive matrix to buffer the volume change during the charge-discharge cycling. Dahn et. al.
• the Sb-MO x -C nanocomposites have been synthesized by a mechanochemical reduction of Sb 2 O 3 with, respectively, Al, Ti, and Mo in presence of carbon (acetylene black). These composite electrodes exhibit excellent electrochemical cycling performance and rate capability compared to pure Sb in lithium cells.
• the ultrafme Sb particles dispersed in the MO x -C ceramic matrix are characterized by X-ray diffraction (XRD), transmission electron microscopy (TEM), X-ray photoelectron spectroscopy (XPS), and electrochemical charge-discharge measurements including impedance analysis.
• XRD X-ray diffraction
• TEM transmission electron microscopy
• XPS X-ray photoelectron spectroscopy
• electrochemical charge-discharge measurements including impedance analysis.
• the XRD, XPS, TEM, and STEM data reveal that these nanocomposites are composed of uniformly dispersed nanostructured Sb in the amorphous Al 2 O 3 , TiO 2 , or MoO 3 matrix along with conductive carbon.
• FIGURE 1 shows the synthesis process employed to obtain the Sn-TiC-C nanocomposite.
• the Sn-Ti (1 :3 atom ratio) alloy was obtained by heating a mixture of Sn and Ti powders mixed with 20 weight percent carbon (acetylene black) followed by a high energy mechanical milling (HEMM), during which the Ti in Sn-Ti reacted with the carbon to produce TiC and consequently the Sn-TiC-C composite.
• the Sn-Ti (1:3 atomic ratio) alloy powders were obtained by heating a mixture of required amounts of Sn (99.9+%, ⁇ 45 ⁇ m, Aldrich) and Ti (99.8%, ⁇ 45 ⁇ m, Aldrich) powders at 600 0 C in a flowing argon atmosphere for 12 h.
• the Sn- Ti alloy thus obtained was then ground and sieved to obtain particles smaller than 75 ⁇ m.
• the Sn-Ti alloy with ⁇ 75 ⁇ m size was then mixed with required amount of acetylene black and subjected to high energy mechanical milling (HEMM) for 40 hours with a speed of 500 rpm in a vibratory mill at ambient temperature under argon atmosphere to obtain Sn-TiC-C.
• the milling was carried out in a hardened steel vial having a capacity of 80 cm 3 with a ball-to-powder ratio of 20: 1 and ball diameters of 3/8 and 3/16 inch.
• the optimum weight ratio between the Sn-Ti alloy and carbon (acetylene black) was 80 : 20, and all the data in the present disclosure refer to samples prepared with a Sn-Ti : C weight ratio of 80 : 20.
• the samples were then analyzed by energy dispersive spectroscopy (EDS) attached to a JEOL 5610 scanning electron microscope (SEM) to detect any contamination from the steel balls.
• EDS energy dispersive spectroscopy
• SEM scanning electron microscope
• the electrodes for the electrochemical evaluation were prepared by mixing 70 weight percent active material (Sn-TiC-C) powder, 15 weight percent carbon black (Super P), and 15 weight percent polyvinylidene fluoride (PVDF) dissolved in N- methylpyrrolidinone (NMP) to form a slurry, followed by coating on a copper foil, pressing, and drying at 120 0 C for 3 hours under vacuum.
• the electrodes were then assembled into CR2032 coin cells in an Ar-filled glove box using Celgard polypropylene separator, lithium foil as the counter electrode, and 1 M LiPF 6 in ethylene carbonate (EC)/diethyl carbonate (DEC) (1 :1 v/v) electrolyte.
• the discharge-charge experiments were performed galvanostatically at a constant current density of 100 mA/g of active material within the voltage range of 0 - 1.5 V vs. Li/Li + .
• the carbon present in the composite was characterized by Renishaw Raman spectroscopy using a 514 nm laser excitation. Structural changes occurring during the charge-discharge process were assessed by detaching the electrodes from the cell, protecting it with a Kapton tape to prevent contamination from air, and then examining it with ex situ XRD.
• the scanning transmission electron microscopy (STEM) images shown in FIGURE 3 a reveals an average particle size of about 300 nm and a homogeneous distributionof Sn, Ti, and C in the Sn-TiC-C nanocomposite.
• FIGURE 3b shows the transmission electron microscopy (TEM) images of the nanocomposite along with selected area diffraction.
• FIGURE 4a shows STEM images
• FIGURE 5 shows the XRD patterns of the Sn-Ti alloy and the Sn-TiC-C nanocomposite. While Sn-Ti alloy (FIGURE 5a) shows reflections corresponding to Sn 5 Ti 6 (JCPDS No. 18-1390) and SnTi 3 (JCPDS No. 06-0583), the Sn-TiC-C nanocomposite (FIGURE 5b) exhibits broad peaks corresponding to TiC without any detectable peaks corresponding to Sn, confirming the amorphous nature of Sn revealed by the TEM data in FIGURE 3b.
• the Sn-TiC-C nanocomposites were analyzed by X-ray photoelectron spectroscopy (XPS) and Raman spectroscopy. While the Sn 3d 5 /2 and 3d 3 /2 peaks observed, at 484.5 eV and 493 eV, respectively, confirmed the presence of metallic Sn, the Ti 2p 3/2 and 2pi /2 peaks observed, at 455 eV and 461 eV, respectively, confirmed the presence of TiC (FIGURE 7). 34 The TiC was formed by a dealloying of Ti from the Sn 5 Ti 6 and SnTi 3 lattices and reaction with carbon during the HEMM process.
• XPS X-ray photoelectron spectroscopy
• Raman spectroscopy Raman spectroscopy
• the integrated intensity ratio I ⁇ IIQ is an indication of the degree of graphitization.
• a high intensity ratio of 0.9 compared to 0.09 in ordered synthetic graphite indicates a higher degree of disorder in the carbon present in the Sn-TiC-C nanocomposite.
• the combination of TEM, XRD, XPS, and Raman spectroscopic data confirmed the presence of amorphous metallic Sn, amorphous or poorly crystalline TiC, and amorphous carbon in the Sn-TiC-C nanocomposite obtained by the HEMM process.
• the voltage profiles of the Sn-TiC-C nanocomposite are shown in FIGURE 10a.
• the nanocomposite exhibited a first discharge and charge capacity of, 501 and 367 mAh/g, respectively, implying an irreversible capacity loss of 134 mAh/g and a coulombic efficiency of 74 percent in the first cycle.
• the irreversible capacity loss is associated with the reduction of the electrolyte on the active material surface and the formation of solid-electrolyte interfacial (SEI) layer.
• SEI solid-electrolyte interfacial
• the differential capacity plots (DCP) at various cycles were analyzed (FIGURE 10b) to fully understand the discharge-charge process.
• the alloying/dealloying of lithium with Sn and carbon over a potential range of 1.5 to 0.0 V (vs. Li/Li ) yielded Li x Sn (x ⁇ 4.4) alloys and LiyC.
• the DCPs showed broad peaks, which are characteristic of the reaction of amorphous Sn, instead of clear voltage plateaus characteristic of crystalline Sn.
• the electrolyte decomposes at approximately 0.75 V to form an SEI layer on the surface of the active material.
• the metallic Sn is generally expected to aggregate into large tin clusters as the number of cycle increases as has been suggested previously by Courtney and Dahn et al w and identified by Retoux et al n
• the capacity retention is expected to decrease as the electrode is cycled since the large tin regions are more sensitive to cracking and crumbling.
• the DCPs are rather smooth in FIGURE 10b and they overlap with each other after the first cycle, reflecting the excellent reversible nature of the process.
• the presence of a large amount of amorphous TiC along with carbon as a conductive buffer matrix suppresses the aggregation of the Sn atoms and imparts good reversibility.
• DCP differential capacity plots
• the Sn-Ti alloy electrode exhibited a first discharge and charge capacities of, 68 and 29 mAh/g, respectively, which is related mainly to the insertion of lithium into the conducting carbon (Super P).
• the Sn-TiC-C nanocomposite electrode shows excellent cyclability compared to pure Sn. The excellent cyclability is related to the amorphous nature of tin in the Sn-TiC-C nanocomposite, which is consistent with recent reports that amorphous or nanostructured alloy materials give the best capacity retention as they may accommodate the volume changes more homogeneously.
• the coulombic efficiency remains stable, indicating that the TiC + C conductive buffer matrix suppresses the aggregation of the Sn atoms. Also, these buffer materials along with the amorphous morphology of Sn are able to absorb better the volume changes.
• the Sn-TiC-C composite retains a capacity of 383 mAh/g after 300 cycles without any noticeable capacity fade.
• the Sn-TiC-C nanocomposite also exhibits excellent rate capability as shown in the inset in FIGURE 12a. For example, it retains a high capacity of about 320 and 315 mAh/g, respectively, at 3C and 5C rates.
• the cyclabilities of the nanocomposite anodes do not differ significantly on adding Mn 2+ , suggesting that the anode may not be poisoned by Mn 2+ and they may be employed with manganese spinel cathodes in lithium ion cells.
• novel Sn-TiC-C nanocomposite anodes of the present invention offer several advantages: (i) the entire synthesis procedure is simple and it can be easily scaled up; (ii) the nanocomposite is free from the expensive cobalt unlike Sn-Co-C anode commercialized recently by Sony in 2005; (iii) the amorphous tin in the nanocomposite alleviates the pulverization and the growth of Sn grains; (iv) the nanosize nature of all the components present in the Sn-TiC-C nanocomposite is helpful to achieve fast electron and lithium ion conduction; (v) the amorphous TiC and carbon phases act as a buffer to mitigate the aggregation of tin nanoparticles and the volume expansion during the discharge-charge cycles. This type of amorphous Sn-TiC-C nanocomposites has great potential as anode materials in lithium-ion batteries.
• the Sn-TiC-C nanocomposite of the present invention can be synthesized by a facile, inexpensive high energy mechanical milling process and investigated as an anode material in lithium ion cells. Characterization data collected with STEM, TEM, XRD, and XPS reveals an uniform dispersion of amorphous Sn nanoparticles within the conductive, amorphous (or poorly crystalline) TiC + carbon matrix.
• the nanocomposite exhibited superior capacity retention over 300 cycles with a capacity of about 370 mAh/g and a much higher volumetric capacity than a graphite anode.
• the superior electrochemical performance of the nanocomposite electrode is attributed to the amorphous nature of Sn, suppression of Sn grain growth, and buffering effect provided by the conductive TiC + C matrix toward the volume expansion-contraction during cycling.
• the samples were analyzed by energy dispersive spectroscopy (EDS) attached to a scanning electron microscope (SEM); the EDS data indicated a very low Fe concentration of about 0.5 weight percent.
• EDS energy dispersive spectroscopy
• SEM scanning electron microscope
• the phase analysis of the synthesized samples was performed with a Phillips XRD and Cu Ka radiation.
• the morphology, microstructure, and composition of the synthesized powders were examined with a Hitachi S-5500 scanning transmission electron microscope (STEM) and JEOL 2010F transmission electron microscope (TEM). Surface characterizations were carried out with a Kratos X-ray photoelectron spectrometer (XPS) with monochromatic Al Ka source.
• STEM scanning transmission electron microscope
• TEM JEOL 2010F transmission electron microscope
• the electrodes for the electrochemical evaluation were prepared by mixing 70 weight percent active material (Sb-MO x -C) powders, 15 weight percent carbon black (Denka black) as a conducting agent, and 15 weight percent polyvinylidene fluoride (PVDF) dissolved in N- methylpyrrolidinone (NMP) as a binder to form a slurry, followed by coating on a copper foil, pressing, and drying at 120 0 C for 3 hours under vacuum.
• active material Sb-MO x -C
• carbon black carbon black
• PVDF polyvinylidene fluoride
• NMP N- methylpyrrolidinone
• the CR2032 coin cells were assembled in an Ar-filled glove box using Celgard polypropylene as a separator, lithium foil as the counter electrode, and 1 M LiPF 6 in ethylene carbonate (EC)/diethyl carbonate (DEC) (1 :1 v/v) as the electrolyte.
• the discharge-charge experiments were performed galvanostatically at a constant current density of 100 mA/g of active material within the voltage range of 0 - 2 V vs. LiZLi + .
• ex situ XRD data were collected after detaching the electrodes from the cell and covering it with a polyimide tape as a protective film.
• Electrochemical impedance spectroscopic analysis was carried out with a Solartron SI 1260 equipment by applying a 10 mV amplitude signal in the frequency range of 10 kHz to 0.001 Hz.
• the impedance response was measured after different number of charge-discharge cycles, (after 1 and 20 cycles) at 2 V vs. Li/Li + .
• the formation Of MoO 3 instead of the anticipated MoO 2 (in accordance with reaction 3) is due to the higher negative standard free energy for the formation for MoO 3 (-767 kJ/mol) compared to that for MoO 2 (-603 kJ/mol).
• the reduced Sb, MO x , and carbon are homogeneously dispersed in the nanocomposites.
• FIGURE 4b shows the high resolution images of the nanocomposites along with fast Fourier transform (FFT) images corresponding to the selected regions.
• FFT fast Fourier transform
• the crystalline Sb phase is confirmed by the FFT image, which agrees with the XRD data in FIGURE 6. Also, the reduced crystalline Sb phase with a size of 15-20 nm is well surrounded by the amorphous MO x oxide and carbon phases. This homogeneously mixed morphology as shown by the schematic description in FIGURE 2 may be beneficial to provide good electrical contact with the current-collector as well as a buffering effect on the volume expansion-contraction occurring during cycling.
• FIGURE 11a compares the first discharge-charge profiles of all the three Sb-Mo x -C nanocomposites.
• the M Mo nanocomposite exhibits the discharge-charge profiles of both Sb and Sb 2 O 3 together with first discharge and charge capacities of, 765 and 537 mAh/g, respectively, implying an initial coulombic efficiency of 70 percent.
• the inset in FIGURE 11a shows the discharge-charge profiles of the ball milled acetylene black. It exhibits a first discharge capacity of about 200 mAh/g, which decreases approximately to one-third in the following cycles as seen in the inset of FIGURE 11a.
• the expected amounts OfAl 2 O 3 and TiO 2 in the M Al and Ti nanocomposites is, 23 and 26 weight percent, respectively. While Al 2 O 3 is known to be electrochemically inactive, TiO 2 is expected to contribute about 55 mAh/g corresponding to the formation of Li x TiO 2 with x about 0.5.
• the differential capacity plots (FIGURE 1 Ib) of the first cycle were studies for all the three nanocomposites.
• the differential discharge plot shows a broad peak from 1.3 to 0.8 V, which is related to the formation of solid electrolyte interfacial (SEI) layer due to electrolyte decomposition on the surface of the active material.
• SEI solid electrolyte interfacial
• FIGURE 13 presents an ex situ XRD analysis performed on fully lithiated and delithiated electrodes for all the Sb-MO x -C nanocomposites.
• some reinforced ceramic-metal composites are known to exhibit high strength, modulus, and enhanced resistance to fatigue crack growth. 41 ' 42 In this system, the enclosure or dispersion of the fine particles of the electrochemically active Sb metal within or among the ceramic oxide and carbon matrix leads to enhanced capacity retention.
• the inventors studied the cyclability of all the three Sb-MO x -C nanocomposite anodes at 25 0 C in presence of 300 ppm Mn 2+ in the electrolyte, i.e. the experiments were carried out by intentionally adding required amount of anhydrous manganese perchlorate salt to the electrolyte (to give 300 ppm Mn 2+ ) before assembling the cell.
• the cyclabilities of the nanocomposite anodes did not differ significantly on adding Mn 2+ , suggesting that these nanocomposite anodes may not be poisoned by Mn 2+ and they may have potential to be employed with manganese spinel cathodes in lithium ion cells.
• EIS measurements were carried out at 2 V vs. Li/Li + with all the three nanocomposite samples at different cycles such as after 1st cycle and 20th cycle.
• the EIS data were analyzed based on an equivalent circuit given in FIGURE 15a, 44 where R n refers to uncompensated resistance between working electrode and lithium reference electrode, CPE 8 refers to constant phase element of the surface layer, R s refers to resistance of the SEI layer, CPE d i refers to CPE of the double layer, R ct refers to charge transfer resistance, and Z w refers to Warburg impedance.
• the EIS spectrum can be divided into three frequency regions, Le, low, medium to low, and high frequency regions, which correspond, respectively, to cell geometric capacitance, charge transfer reaction, and lithium ion diffusion through the surface layer.
• the EIS spectra recorded after 1st and 20th cycles in FIGURE 15b consist of one semicircle and a line.
• the diameter of the semicircle is a measure of the charge transfer resistance R cU which is related to the electrochemical reaction between the particles or between the electrode and the electrolyte.
• the sloping line is related to lithium ion diffusion in the bulk of the active material.
• the diameter of the semicircle increases on going from 1st to 20th cycle, indicating an increase in R ct as the electrode is cycled, possibly due to the breaking of the inter-particle contact caused by the volume expansion.
• the buffering effect provided by the amorphous metal oxide and conductive carbon matrix mitigates the problems normally encountered with the volume changes occurring during cycling and leads to good electrochemical performance.
• the disclosure demonstrates that the problems normally encountered with the huge volume expansion associated with the alloy anodes could be minimized by a rational design of nanocomposite microstructures as described in the present invention.
• compositions of the invention can be used to achieve methods of the invention.
• the words “comprising” (and any form of comprising, such as “comprise” and “comprises”), “having” (and any form of having, such as “have” and “has”), "including” (and any form of including, such as “includes” and “include”) or “containing” (and any form of containing, such as “contains” and “contain”) are inclusive or open-ended and do not exclude additional, unrecited elements or method steps.
• A, B, C, or combinations thereof refers to all permutations and combinations of the listed items preceding the term.
• A, B, C, or combinations thereof is intended to include at least one of: A, B, C, AB, AC, BC, or ABC, and if order is important in a particular context, also BA, CA, CB, CBA, BCA, ACB, BAC, or CAB.
• expressly included are combinations that contain repeats of one or more item or term, such as BB, AAA, MB, BBC, AAABCCCC, CBBAAA, CABABB, and so forth.
• the skilled artisan will understand that typically there is no limit on the number of items or terms in any combination, unless otherwise apparent from the context.
• compositions and/or methods disclosed and claimed herein can be made and executed without undue experimentation in light of the present disclosure. While the compositions and methods of this invention have been described in terms of preferred embodiments, it will be apparent to those of skill in the art that variations may be applied to the compositions and/or methods and in the steps or in the sequence of steps of the method described herein without departing from the concept, spirit and scope of the invention. All such similar substitutes and modifications apparent to those skilled in the art are deemed to be within the spirit, scope and concept of the invention as defined by the appended claims.

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• 2010
  • 2010-05-27 WO PCT/US2010/036469 patent/WO2010138760A2/en active Application Filing
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